Devices, systems and methods for endovascular temperature control

ABSTRACT

Devices, systems and methods for controlling a patient&#39;s body temperature by endovascular heat exchange.

RELATED APPLICATION

This is a continuation in part of copending U.S. patent application Ser. No. 15/423,581 entitled Devices, Systems and Methods for Endovascular Temperature Control filed Feb. 2, 2017, the entire disclosure of which is expressly incorporated herein by reference.

FIELD OF THE INVENTION

The present disclosure relates generally to the fields of medicine and engineering and more particularly to devices, systems and methods for controlling a patient's body temperature by endovascular heat exchange.

BACKGROUND

Pursuant to 37 CFR 1.71(e), this patent document contains material which is subject to copyright protection and the owner of this patent document reserves all copyright rights whatsoever.

In various clinical situations, it is desirable to warm, cool or otherwise control the body temperature of a subject. For example, hypothermia can be induced in humans and some animals for the purpose of protecting various organs and tissues (e.g., heart, brain, kidneys) against the effects of ischemic, anoxic or toxic insult. For example, animal studies and/or clinical trials suggest that mild hypothermia can have neuroprotective and/or cardioprotective effects in animals or humans who suffer from ischemic cardiac events (e.g., myocardial infract, acute coronary syndromes, etc.), postanoxic coma after cardiopulmonary resuscitation, traumatic brain injury, stroke, subarachnoid hemorrhage, fever and neurological injury. Also, studies have shown that whole body hypothermia can ameliorate the toxic effects of radiographic contrast media on the kidneys (e.g., radiocontrast nephropathy) of patients with pre-existing renal impairment who undergo angiography procedures.

One method for inducing hypothermia is by endovascular temperature management (ETM) wherein a heat exchange catheter is inserted into a blood vessel and a thermal exchange fluid is circulated through a heat exchanger positioned on the portion of the catheter that is inserted in the blood vessel. As the thermal exchange fluid circulates through the catheter's heat exchanger, it exchanges heat with blood flowing past the heat exchange in the blood vessel. Such technique can be used to cool the subject's flowing blood thereby resulting in a lowering of the subject's core body temperature to some desired target temperature. ETM is also capable of warming the body and/or of controlling body temperature to maintain a monitored body temperature at some selected temperature. If a controlled rate of re-warming or re-cooling from the selected target temperature is desired, that too can be accomplished by carefully controlling the amount of heat added or removed from the body and thereby controlling the temperature change of the patient.

SUMMARY

In accordance with the present disclosure, there are provided heat exchange devices, systems and methods which facilitate efficient endovascular and/or body surface heat exchange.

In accordance with one embodiment, there is provided a system for circulating a warmed or cooled thermal exchange fluid through an endovascular heat exchanger (e.g., an endovascular heat exchange catheter), wherein a) the system produces a pulsatile flow of thermal exchange fluid and b) the system is connected to the endovascular heat exchanger by way of one or more conduits which comprise a pulse damping conduit that functions not only as a conduit through which the thermal exchange fluid flows but also a pulse damper for damping pulses or pressure in the thermal exchange fluid as it flows therethrough. The pulse damping conduit may comprise, for example, tubing that has sufficient elastic or flexural properties to dampen or reduce the amplitude of pulses in the thermal exchange fluid as it flows therethrough.

In accordance with another embodiment, there is provided a system for warming or cooling the body of a human or animal subject, such system comprising an extracorporeal control system that is connectable to one or more changeable component(s) (e.g., an endovascular heat exchange catheter, a body surface heat exchange pad, tubing, a cassette through which thermal exchange fluid circulates, other disposable components, etc.). When the changeable component(s) is/are connected to the extracorporeal control system, the system is useable to effect heat exchange with the subject's body. The changeable component(s) may include machine readable encoded information. The extracorporeal control system includes a reader that receives and reads the encoded information. The extracorporeal control system uses such encoded information to identify, qualify, confirm or control the operation of the changeable component(s). The encoded information may be stored in any suitable electronic storage medium and may be embedded in a chip or microchip mounted on or in the changeable component(s). Examples of the types of encoded information that may be stored include but are not limited to; unique identifier(s) for the changeable components (e.g., manufacturer identification, part number, lot number, etc.), indications of whether the changeable component(s) have previously been used (e.g., an encoded indication of first use), indications of whether the changeable component(s) is/are expired (e.g., encoded expiration date), operational characteristic(s) of the changeable component(s) (e.g., encoded indications of the size, type, volume, etc. of the changeable component(s). Examples of the types of information storage that may be utilized include but are not necessarily limited to: non-volatile random access memory (RAM), non-volatile flash memory, electrically erasable programmable read-only memory (EEPROM) or ferroelectric random access memory (FRAM). The extracorporeal control system may comprises a controller (e.g., a processor) programmed to take one or more actions in response to the encoded information. For example, the controller may be programmed to determine whether the encoded information meets a prerequisite requirement and to proceed with warming or cooling of the subject's body only if said prerequisite requirement is met.

In accordance with another embodiment, there is provided a thermal exchange engine for warming or cooling a thermal exchange fluid. Such thermal exchange engine comprises thermal exchange plates or evaporators which are alternately coolable by circulation of refrigerant through the plates and warmable by heaters positioned on or in the plates. A cassette receiving space is located between the temperature controlled plates and is configured for receiving a cassette or heat exchanger. The cassette comprises a frame and an expandable vessel (e.g., a bag or other expandable fluid containing vessel). The expandable vessel is fillable with thermal exchange fluid, e.g., after the cassette has been inserted into the cassette receiving space. Heat is thereby transferred between the refrigerant and the thermal exchange fluid or the heater(s) and the thermal exchange fluid. In some embodiments, outer surface(s) of the expandable vessel may be coated with a release material, covered with a layer of releasable material or otherwise treated or modified to deter sticking of the expandable vessel to the adjacent thermal exchange plates. In some embodiments, surface(s) of the thermal exchange plates and/or surfaces of the expandable vessel or a layer on a surface of the expandable vessel may be textured or provided with holes, groves or other surface features to deter sticking of the expandable vessel to the adjacent thermal exchange plates. In some embodiments, the cassette may comprise a housing attached to an insertable portion (e.g., the frame and expandable vessel) by a hinged attachment such that the cassette may be disposed in a folded or dosed configuration prior to use and converted to an unfolded or open configuration at the time of use. Such hinged connection between the housing and the insertable portion may be constructed so that, once unfolded or opened, the cassette locks in the unfolded or open configuration. In some embodiments, a plurality of hooks located in the console or system may be initially positioned in retracted positions allowing insertion of the instertable portion into the cassette receiving space between the thermal exchange plates and, thereafter, may be moved to advanced positions wherein they hold the insertable portion of the cassette within the cassette receiving space.

In accordance with another embodiment, there is provided a system configured to circulate warmed or cooled thermal exchange fluid through a body heat exchanger to warm or cool the body or a human or animal subject, wherein the system comprises a first display device which receives signals from one or more temperature sensors and displays temperature data based on signals received from said one or more temperature sensors. The first display device is connectable, by wired or wireless connectivity, to a second display device (e.g., a bedside monitor, central unit monitor, remote monitor, etc.), so as to transmit said signals received from said one or more temperature sensors from the first display device to the second display device. The system further comprises circuitry for minimizing or eliminating any effect of ambient temperature on such signals as they are transmitted from the first display device to the second display device. In some embodiments, the signals transmitted from the first display device to the second display device may comprise signals representative of sensed temperatures, such as patient body temperature, temperature of thermal exchange fluid flowing to the body heat exchanger, temperature of thermal exchange fluid flowing from the body heat exchanger, etc.

Still further aspects and details of the present invention will be understood upon reading of the detailed description and examples set forth herebelow.

BRIEF DESCRIPTION OF THE DRAWINGS

The following detailed description and examples are provided for the purpose of non-exhaustively describing some, but not necessarily all, examples or embodiments of the invention, and shall not limit the scope of the invention in any way.

FIG. 1 shows one embodiment of an endovascular heat exchange system comprising an endovascular heat exchange catheter, an extracorporeal control console and a tubing/cassette/sensor module assembly useable for operatively connecting the heat exchange catheter to the control console.

FIG. 2A is a left/front perspective view of the control console with its access cover in an open position.

FIG. 2B is a left/rear perspective view of the control console.

FIG. 3 is an exploded view of the control console with its access cover in an open position and the tubing/cassette/sensor module assembly staged for insertion in, and operative connection to, the control console.

FIG. 4 is a top (perspective) view of the control console with its access cover in an open position and the tubing/cassette/sensor module assembly operatively inserted in and connected to the control console.

FIG. 5 is a top (plan) view of the control console with its access cover in an open position and the tubing/cassette/sensor module assembly operatively inserted in and connected to the control console.

FIG. 6 is a right/front perspective view of the control console with its housing and access cover removed.

FIG. 7 is a left cross-sectional view of the control console.

FIG. 8 is a top cross-sectional view of the control console.

FIG. 9 is a right cross-sectional view of the control console.

FIG. 10 is a perspective view of a thermal exchange engine component of the control console.

FIG. 11 is a bottom/perspective view of a thermal exchange plate assembly of the thermal exchange engine.

FIG. 12 is a top/perspective view of the thermal exchange plate assembly.

FIG. 13 is a top (plan) view of the thermal exchange plate assembly of the thermal exchange engine.

FIG. 14 is disassembled view of one of the thermal exchange plates of the thermal exchange plate assembly, exposing a vertically oriented serpentine refrigerant flow path formed in the inner surface of the plate.

FIG. 15 is a rear view of the thermal exchange plate assembly with the outer plate and heater removed.

FIG. 16 is a partially disassembled rear perspective view of with the thermal exchange plate wherein rear plates have been removed so as to expose secondary fluid flow channels useable for optional non-cassette warming/cooling of a fluid.

FIG. 17 is a top view of the fully assembled thermal exchange plate assembly.

FIG. 18 is a schematic diagram illustrating the functional lay out of the thermal exchange engine.

FIG. 19 is a front perspective view of the pump assembly of extracorporeal control console.

FIG. 20 is a partially disassembled view of the pump assembly wherein the cover has been removed.

FIG. 20A is a separate view of a barrel-shaped guide roller of the pump assembly.

FIG. 21 is a top view of the pump assembly. 10036 j FIG. 22 is a rear perspective view of the pump assembly disposed in an operative configuration.

FIG. 23 is a rear perspective view of the pump assembly disposed in a loading configuration.

FIG. 24 is a rear perspective view of the tubing/cassette/sensor module assembly of the endovascular heat exchange system.

FIG. 25 is a front perspective view of the tubing/cassette/sensor module assembly.

FIG. 26 is a side view of the cassette and pump tubing portions of the tubing/cassette/sensor module assembly disposed in an open/locked configuration useable for insertion and operation.

FIG. 27 is a rear perspective view of the cassette and pump tubing portions of the tubing/cassette/sensor module assembly disposed in a closed configuration prior to insertion and operation.

FIG. 28 is a cross sectional view of the cassette portion of the tubing/cassette/sensor module assembly.

FIG. 29 is an exploded view of the sensor module portion of the tubing/cassette/sensor module assembly.

FIG. 30 is a schematic diagram of an endovascular heat exchange system. (convert to black/white formalize)

FIG. 31 is a schematic diagram of a heat exchange system capable of providing endovascular and/or body surface heat exchange.

FIG. 32 shows the heat exchange catheter of the system of FIG. 1.

FIG. 32A is a cross-sectional view through line A-A of FIG. 32.

FIG. 32B is a cross-sectional view through line B-5 of FIG. 32.

FIGS. 33A through 33C show certain components of the endovascular heat exchange catheter embodiment of FIG. 32. Specifically, FIG. 33A is a side view of the elongate member; FIG. 33B is a side view of the heat exchange tube and FIG. 33C is a side view of an optional elongate luminal member and the distal tip member.

FIG. 34 is a flow diagram showing one example of a process by which a body heat exchange system may employ hot refrigerant from its cooling engine to augment the warming effect of resistance heaters.

FIG. 35 is a flow diagram showing one example of a process by which a body heat exchange system may combine variations in heat exchange fluid flow rate with variations in heat exchange fluid temperature for precise maintenance of a target body temperature.

FIG. 36 is a flow diagram showing one example of a process by which a body heat exchange system may optimize pump speed and heat exchange fluid pressure during operation with either warm or cool heat exchange fluid.

FIG. 37 is a flow diagram showing one embodiment of a process for using a heat exchange catheter system to deter reperfusion injury in a subject who is suffering from an ischemic event that is treatable by a reperfusion procedure or administration of a reperfusion agent (e.g., thrombolytic drug).

DETAILED DESCRIPTION

The following detailed description and the accompanying drawings to which it refers are intended to describe some, but not necessarily all, examples or embodiments of the invention. The described embodiments are to be considered in all respects only as illustrative and not restrictive. The contents of this detailed description and the accompanying drawings do not limit the scope of the invention in any way.

FIG. 1 shows one embodiment of an endovascular heat exchange system 10 in operation to control the body temperature of a human subject. This endovascular heat exchange system 10 generally comprises an endovascular heat exchange catheter 12, an extracorporeal control console 14, a tubing/cassette/sensor module assembly 60 or cassette assembly which facilitates connection of the catheter 12 to the control console 14 and a temperature sensor TS. In at least some embodiments, the catheter 12, tubing/cassette/sensor module assembly 60 or cassette assembly and temperature sensor TS may be disposable items intended for a single use, while the control console 14 may be a non-disposable device intended for multiple uses.

In the embodiment shown, the endovascular heat exchange catheter 12 comprises an elongate catheter body 16 and a heat exchanger 18 positioned on a distal portion of the catheter body 16. Inflow and outflow lumens (not shown) are present within the catheter body 16 to facilitate circulation of a thermal exchange fluid (e.g., sterile 0.9% sodium chloride solution or other suitable thermal exchange fluid) through the heat exchanger 18. Optionally, the catheter shaft 16 may also include a working lumen (not shown) which extends through the catheter body 16 and terminates distally at an opening in the distal end of the catheter body 16. Such working lumen may serve as a guidewire lumen to facilitate insertion and position of the catheter 12 and/or may be used after insertion of the catheter 12 for delivery of fluids, medicaments or other devices. For example, as shown in FIG. 1, in some embodiments, the temperature sensor TS may be inserted through the catheter's working lumen and advanced out of the distal end opening to a location beyond the distal end of the catheter body 16. Alternatively, in other embodiments, the temperature sensor TS may be positioned at various other locations on or in the subject's body to sense the desired body temperature(s). Various heat exchange catheters may be used in the embodiments described herein.

With reference to FIGS. 32 through 33C, the elongate body 16 of the catheter 12 may comprise a proximal body 1300 and an assembly 1302 which comprises the heat exchanger 1304 attached to and/or extending distally from the proximal body 1300. As seen in the cross sectional view of FIG. 32B, in this particular embodiment, the proximal body 1300 has three lumens, an inflow lumen 1500 a, an outflow lumen 1500 b and an optional through lumen 1500 c.

A hub 1700 is mounted on the proximal end PE of the proximal catheter body 1300. The hub 1700 has an inflow connector 30000 that is connected to the inflow lumen 1500 a of the catheter body 1300 and an outflow connector 32000 that is connected to the outflow lumen 1500 b of the proximal catheter body 1300. A through lumen port 2200 on the hub 1700 is connected to the through lumen 1500 c.

The heat exchanger 1304 of this catheter embodiment comprises at least first and second coiled heat exchange tube segments 1307 a, 1307 b. In some embodiments, additional (e.g., third, fourth) heat exchange tube segments may be used. The heat exchange tube segments 1307 a, 1307 b may be formed of any suitable material. In the particular example shown, the heat exchange tube segments 1307 a, 1307 b may be advantageously formed of a noncompliant polymeric material, such as polyethylene terephthalate (PET), Pebax, Polyolefin, Polyurethane and/or Nylon, or other suitable compliant or noncompliant material and may be formed of a single tube or one or more tubes. In some embodiments the heat exchange tube segments 1307 a, 1307 b may expand and collapse depending on whether or not they are filled with fluid and, in such embodiments, the heat exchange tube segments 1307 a, 1307 b may be referred to a “balloons.” For some applications, the heat exchange tube segments 130 fa, 1307 b may have outer diameters in the range of 2 mm-19 mm and wall thicknesses in the range of 0.0127 mm-0.1 mm.

In this example, the proximal end of the first tube segment 1307 a is connected to the inflow lumen 1500 a and the proximal end of the second tube 1307 b segment is connected to the outflow lumen 1500 b. The distal ends of the first and second tube segment 1307 a, 1307 b are directly or indirectly in fluidic connection with each other such that heat exchanger fluid that has flowed in the distal direction through the first tube segment 1307 a will then return in the proximal direction through the second tube segment 1307 b. The distal ends of the heat exchange tube segment 1307 a, 1307 b are connected to the inflow and outflow connectors 30000, 32000 of the catheter 12.

As seen in detail in FIGS. 33A-33C, the heat exchange assembly 1302 may comprise a spine or elongate member 4000 and at least one heat exchange member 1307 disposed on the spine or elongate member 4000. The heat exchange assembly 1302 is attached to and extends distally from the proximal body 1300, as shown. An introducer sheath may be used to introduce the catheter into a patient's body. Alternatively, the catheter may be introduced without using an introducer sheath.

The term “elongate member,” may mean, in at least some embodiments, a member, e.g., a spine or similar structure, which extends from a catheter body and upon which at least one heat exchange member is disposed. In at least some embodiments, the elongate member 4000 is distinguishable from the proximal body 1302 on the basis of one or more differences in structure or physical property. In the particular embodiment shown, the elongate member 4000 comprises an elongate, generally C-shaped member having receiving features 4600 which comprise spaced-apart transverse notches, recesses or grooves formed along the open side of the generally C-shaped member. The heat exchange member(s) 1307 may be inserted in these recessed, groove, or notch-type receiving features 4600 such that the helical loops extend around the closed side of the generally C-shaped elongate member 4000. The heat exchange member(s) 1307 may be secured to the receiving features 4600 by adhesive or other suitable means.

Non-limiting examples of other heat exchange catheters and related apparatus that may be used are described in U.S. Pat. No. 9,492,633, and United States Patent Application Publications Nos. 2013/0090708, 2013/0178923, 2013/0079855, 2013/0079856, 2014/0094880, 2014/0094882, 2014/0094883, and unpublished, copending U.S. patent application Ser. Nos. 15/395,858, 15/395,923 and 15/412,390, the entire disclosure of each such patent and application being expressly incorporated herein by reference. Other examples of catheters that may be used in this invention include those commercially available from ZOLL Circulation, Inc., San Jose, Calif., such as the Cool Line® Catheter, Icy® Catheter, Quattro® Catheter, Solex 7® Catheter, InnerCool® RTx Accutrol Catheter and the InnerCool RTx Standard Catheter. Additionally incorporated herein by reference is the entire disclosure of U.S. patent application Ser. No. 15/594,539 entitled Advanced Systems and Methods for Patent Body Temperature Control, filed on May 12, 2017.

The extracorporeal control console 14 generally comprises a main housing 20 and a console head 24. As described in detail herebelow, the main housing 20 contains various apparatus and circuitry for warming/cooling thermal exchange fluid to controlled temperature(s) and for pumping such warmed or cooled thermal exchange fluid through the catheter 18 to effectively modify and/or control the subject's body temperature. The console head 24 comprises a display device or user interface, such as a touch screen system, whereby certain information may be input by, and certain information may be displayed to, users of the system 10. On the housing 20 there are provided a first connection port 40 for connection of a temperature sensor TS that is inserted through the heat exchange catheter 12 as shown in FIG. 1 as well as other connection ports 36, 38 for connection of additional or alternative types of temperature sensors and/or other apparatus.

The tubing/cassette/sensor module assembly 60 or cassette assembly, which is seen in further detail in FIGS. 3-5, generally comprises a sensor module 34, an inflow conduit 32, inflow connector 33, outflow conduit 30, outflow connector 31, temperature lead TL, temperature lead connector 35, pressure lead PL, cassette 64, cassette housing 62 and peristaltic pump tubing 65.

FIGS. 2A through 9 show further detail of the components within the housing 20 and the manner in which the tubing/cassette/sensor module assembly 60 or cassette assembly is inserted in and connected to the control console 14. As seen in FIGS. 2A through 3, the control console 14 has an openable/closable access cover 42 which, when opened, permits insertion of the cassette 64 into a cassette receiving space 66 as well as other connection of the tubing/cassette/sensor module assembly 60 or cassette assembly to other components of the system described below. A magnet 44 on the access cover 42 interacts with a magnetic sensor 46 to emit signal(s) indicating whether the access cover 42 is opened or closed. Other sensors and detection mechanisms known to persons having skill in the art may be utilized as well. The system controllerlocated in the housing 20 may be programmed to halt running of certain components of the system when the access cover 44 is opened. On the rear of the housing 20, there is provided a power switch 50 and a power cord holder 52. A bracket 48 is provided on an upstanding portion of the housing which supports the console head 24 for hanging a bag or container of fluid.

As seen in FIGS. 3 through 5, with the access cover 42 in an open position, the cassette 64 is insertable downwardly into the cassette receiving space 66 and the pump tubing 65 is insertable into a tubing raceway 72 of pump 70.

FIGS. 6 through 10 provide partially disassembled and sectional views which reveal various components of the control console 14. The thermal exchange engine 108, includes a refrigeration system which comprises a compressor 92, stepper motor for turning an expansion valve 106, fans 96 and 104, condenser 98 and compressor heat sink 100. The heat sink may be a metallic, e.g., aluminum, cylindrical enclosure that surrounds the compressor. The heat sink is in contact with the compressor and increases the surface area of the compressor to facilitate enhances removal of heat from the compressor. The thermal exchange system is powered by power supply 94. Thermal exchange plates 80, are provided to alternately warm or cool thermal exchange fluid as it circulates through a cassette 64 that has been inserted in the cassette receiving space 66 between the thermal exchange plates. Resistance heaters 82 are mounted on the plates 80 for warming the plates 80 when operating in a warming mode and a refrigerant, such as Refrigerant R143a (1, 1, 1, 2 Tetrafluoroethane) is compressed by the compressor 92 and circulated through the condenser 98 and plates 80 to cool the plates when operating in a cooling mode. In certain embodiments, heaters may include a thermal cutout switch for automatically turning one or more of the heaters off if the heaters were to overheat.

When operating in a cooling mode, the thermal exchange engine 108 emits heat. Fans 96 and 104 circulate air through air plenums or spaces adjacent to the thermal exchange engine 108 and over surfaces of the compressor and compressor heat sink 100 to exhaust emitted heat and maintain the thermal exchange engine 108 at a suitable operating temperature. Specifically, in the embodiment shown, air enters air intake 84 through filter 90, circulates through the device as indicated by arrows on FIGS. 7 and 8, and is exhausted through an air outlet or exhaust vent on a side of the console 14 as shown specifically in FIG. 8. The airflow pathway is specifically configured to minimize the amount of sound that escapes from the system via the airflow pathway and is audible to a user or patient. The airflow pathway includes a convoluted pathway or channels which provide reflective surfaces to contain the acoustic energy within the cooling engine enclosure. Also, the interior of the intake and exhaust ducts and pathway or channels are lined with an acoustically absorbent material, e.g., open-celled elastomeric foam. The combination of these features minimizes the amount of sound, such as that generated by the fans and compressor, that escapes the system. For example, in certain embodiments, the operating noise level of a system may not exceed 65 dBA measured at a distance of 1 m from the system when the system is in maximum cooling and 58 dBA measured at a distance of 1 m from the system when the system is in maintenance or warming.

The structure and function of the thermal exchange plates may be appreciated in further detail in FIGS. 11 through 17. Thermal exchange plates 80 may be positioned on either side of the cassette receiving space 66. The thermal exchange plates are connected on their ends forming a cassette receiving space or slot between the plates. The thermal exchange plates may be referred to as a thermal exchange plate assembly. Resistance heaters 82 are mounted in one or more of plates 80 and are useable to warm the plates 80 when warming of the circulating thermal exchange fluid is desired. In certain embodiments, vertically oriented, serpentine or convoluted, refrigerant flow channels 120 are formed within the plates 80. This orientation and design of the refrigerant flow channels help maximize and realize the cooling power of the cooling engine, For example, the plates are configured to evaporate the refrigerant moved by a 900 W compressor (e.g., a Masterflux compressor) within a cooling engine envelope sized to fit within the housing 20, as illustrated in the figures herein. In each plate, cold refrigerant circulates through refrigerant inlet 112, through the refrigerant flow channels 120 and out of refrigerant outlet 114. The refrigerant changes phase from a liquid substantially to a gas while flowing through the refrigerant flow channels 120, thereby cooling the plates 80. Such warming or cooling of the plates 80, in turn causes warming or cooling of thermal exchange fluid being circulated through a cassette positioned within the cassette receiving space 66. Temperature sensors 110, e.g., thermistors, may be located on the plates to detect the temperature of the plates. Signals from the temperature sensors may be fed back to the system controller or control processor to control warming and/or cooling (e.g., to prevent freezing) by the system.

Optionally, as shown in the views of FIGS. 15 and 16, the thermal exchange plates 80 may incorporate channels 125 for circulation of a thermal exchange fluid directly through the plates. For example, a desired thermal exchange fluid may circulate in inlet 122, through horizontal flow channels 125 and out of outlet 124. A single inlet port may be used to supply thermal exchange fluid to both plates as the fluid passes from a first plate to the second plate, through channels located at the ends of the thermal exchange plate assembly, and exits the thermal exchange plate assembly through a single outlet port. A drain port 127 may be provided for draining residual thermal exchange fluid or flushing debris from the flow channels 125, when required. These channels 125 may be used for cooling or warming a secondary thermal exchange fluid simultaneously with, or as an alternative to, the warming or cooling of a heat exchange fluid circulating through a cassette 64 inserted within the cassette receiving space 66. In some embodiments, the channels 125 may be configured to provide a volume flow of secondary thermal exchange fluid that differs from the volume flow of thermal exchange fluid which circulates through the cassette 64. For example, a cassette 64 may be inserted in the cassette receiving space 66 and used for circulating a relatively small volume of warmed or cooled thermal exchange fluid (e.g., sterile saline solution) through an endovascular catheter 12 and, simultaneously or alternately, the channels 125 may be used to warm or cool a larger volume of a secondary thermal exchange fluid (e.g., nonsterile water) for circulation through body surface cooling device(s) such as surface cooling pad(s), blanket(s), garment(s), etc. Further details and examples of such concurrent or separate use of endovascular and body surface temperature exchange are described in copending U.S. patent application Ser. No. 15/412,390 entitled Managing Patient Body Temperature Using Endovascular Heat Exchange in Combination With Body Surface Heat Exchange, the entire disclosure of which is expressly incorporated herein by reference.

A schematic diagram of an embodiment of a thermal exchange engine or refrigeration loop useable in the systems described herein is shown in FIG. 18. This embodiment has a high side HS and a low side LS. The components shown in this diagram include superheat temperature sensor 130, thermal exchange plate evaporators 132, electric heaters 134, an electronic expansion valve, compressor 140, counterflow heat exchanger 142, filter/drier sight glass 138, and electronic expansion valve 144. In the normal operational state of the cooling engine, the hot gas bypass valve 136 is closed, the compressor 140 is running, and refrigerant flows through the system as follows. First, refrigerant exits the compressor in the gaseous phase at high pressure (typically 8-14 bar) and high temperature (typically 100 to 130 degrees F.) and enters the condenser. In the condenser, heat is transferred from the refrigerant, causing it to condense into it's liquid phase and cool further (typically to 75-95 degrees F.). Liquid refrigerant then passes through the filter dryer 138 which filters the liquid for particulate and absorbs any water contained in the liquid. From there, liquid refrigerant passes the sight glass “S” which allows an observer (e.g. service person) to confirm the refrigerant is in the liquid phase. Liquid refrigerant then passes through the primary channel of the counterflow heat exchanger 142, which causes it to cool further (typically to 40-75 degrees F.) due to heat transfer with the secondary channel of the counterflow heat exchanger. From there, liquid refrigerant passes through the expansion valve 144, which acts as a restriction on the system. After passing through the expansion valve, refrigerant is suddenly at low pressure (typically 2-4 bar) and as a result drops in temperature (to typically 25-35 degrees F.) and partially enters the gaseous phase. Cold, low-pressure, liquid refrigerant then enters the heat exchange plates 132. Heat is added to the refrigerant from the following sources: from the thermal mass of the plates, from saline passing through the cassette heat exchanger, or from water passing through the liquid channels within the cold plates, all of which cause the refrigerant to mostly or entirely enter the gas phase. From the heat exchange plates 132, low-pressure refrigerant flows into the secondary channel of the counterflow heat exchanger where it transfers heat from the refrigerant contained in the primary channel, causing it to warm (to typically 35 to 70 degrees F.). Refrigerant at this point may be mostly or entirely in the gas phase, and then enters the compressor 140, thus completing the circuit. A secondary operational state exists for the cooling engine, where the HGBP valve 136 is open. In this state, hot, gaseous refrigerant exits the compressor and directly enters the heat exchange plates, causing them to warm up rapidly. This secondary state is used when it is desirable to slow down the cooling provided to the patient, or to warm the patient, without turning off the compressor. Alternatively, the compressor can be shut off, however use of the HGBP valve 136 has the advantage of being able to be opened and closed rapidly and repeatedly as necessary to maintain the desired heat exchange plate temperature. One embodiment of a pump 70 (e.g., a peristaltic pump) and associated assembly is shown in FIGS. 19 through 23. The pump 70 comprises a rotor assembly 160 and cover 161 connected to a drive motor 170 which causes the rotor assembly to rotate. The rotor assembly includes guide rollers 164 a and 164 b, and drive rollers 166 a and 166 b. As the rotor assembly rotates, during pump operation, the drive rollers apply pressure to the pump tubing (not shown), which is positioned in the pump raceway, thereby causing thermal exchange fluid to move through the pump tubing. The pump raceway is designed with a low height (i.e. as measured along the axes of the rollers) in order to allow the pump to be smaller, lighter weight, and lower cost. However with this low height it is critical to keep the pump tubing aligned with the raceway, in order to avoid jamming of the tubing within the pump assembly (leading to wear of the pump and wear or rupture of the tubing), and to avoid the tubing partially or entirely coming out of contact with the drive rollers and thereby not generating some or all of the pressure needed to pump heat exchange fluid through the catheter. As seen in FIG. 20A, each guide roller 164 a, 164 b has a tapered (e.g., barrel shaped) side wall 165. The guide roller may include a central section which is not tapered (i.e. parallel to the axis of rotation) 167. The tapered or barrel shape of the guide roller facilitates self-centering of the pump tubing on the guide roller, to ensure that the pump continues to perform as intended. Because the tubing is being stretched over the guide rollers, a normal force is generated, which in turn creates a frictional force. The taper on the rollers is at a shallow angle (e.g., of a range of 5 to 25 degrees) so that the frictional force is sufficient to prevent the tubing from sliding on the roller surface. Given that the tubing does not slide, the taper or barrel shape puts a higher tensile load on the pump tubing at the center of the roller (i.e. at the widest part of the barrel or roller), and a lower tensile load on the pump tubing at either the top or bottom edges of the roller (i.e. the narrowest part of the barrel or roller). This difference in tensile forces leads to the self-centering effect by developing a net force acting on the tubing along the axis of the roller, in the direction of the center of the roller. A front portion of the pump 70 is mounted on a front plate 172. Optical sensors 174, for detecting when a cassette 64 and its cassette housing 62 are in place and properly positioned for operation, may also be located on the front plate 172. Hooks 176 a, 176 b extend through slots in the front plate 172. These hooks 176 a, 176 b are positionable in retracted positions which allow installation of the cassette 64 and insertion of the pump tubing 65 in the pump raceway 162. Thereafter, these hooks 176 a and 176 b are movable to advanced positions wherein they exert a force on the cassette housing 62 at two separate points of contact thereby deterring unwanted movement of the cassette 64, cassette housing 62 or attached pump tubing 65, and securing the cassette in position for system operation. Also mounted on the front plate 172 are level sensors for sensing fluid levels within a reservoir formed within the cassette housing 62. The pump 70 is alternately disposable in an operative configuration (FIG. 22) and a loading configuration (FIG. 23). Translational motor 180 causes the hooks to move between a retracted and advanced position, and causes the pump to move between an operative and loading configuration or position.

Priming of the system, when the cassette 64 is positioned in the cassette receiving space 66 between thermal exchange plates 80, may be performed quickly by using one or more pump direction changes. The pump 70 may be switched back and forth between running in reverse and running in a forward direction for various durations of time, at various speeds. The first pump reversal creates a vacuum and the subsequent reversals help remove bubbles from the system/line.

To purge the thermal exchange fluid from the system the pump 70 may be run in reverse. In one example, the pump 70 may be run in reverse at 60% of max pump speed for about 20 seconds, during which the return line or vessel outlet line is closed to prevent the cassette vessel/bag from refilling with thermal exchange fluid or saline when the pump is reversed or opened. A check valve may be utilized, which may be positioned in the cassette housing, e.g., in the vessel outlet tubing, between the tubing and the reservoir, to prevent the vessel/bag from refilling with thermal exchange fluid or saline when the pump is reversed or open. For example, in some embodiments, the check valve may be integrated into the inflow connector 206 seen in FIG. 28 to prevent fluid from back-flowing into the vessel/bag 63 when the pump is reversed or open.

FIGS. 24 through 28 show further details of the tubing/cassette/sensor module assembly 60 or cassette assembly. The cassette housing 62 is attached to a frame 69 which supports the side edges of the expandable vessel or bag 63. A lower edge 63 a of the expandable vessel or bag is sealed and may include a support. As seen in FIG. 28, the cassette housing (bottom cover removed) 62 encloses a reservoir 206, pressure sensor 202, outflow connector 204 which is connected to the pulse-damping outflow conduit 30, inflow connector 206 which is connected to return or inflow conduit 32. During system operation, thermal exchange fluid returns from the catheter, flowing through inflow conduit 32, through inflow connector 206, through vessel inlet tubing, into the expandable vessel or bag 63, through the expandable vessel or bag 63 from one side to the other as indicated by arrows on FIG. 28, exchanging heat with refrigerant flowing through the thermal exchange plates, then out of the vessel through vessel outlet tubing, into reservoir 206, through pump tubing 65, through outflow connector 204, through pulse-damping outflow conduit 30 and back to the catheter. Refrigerant flows through the refrigerant flow channels in the thermal exchange plates in a first direction, while thermal exchange fluid flows though the expandable vessel in a second direction that is substantially opposite the first direction. This counter flow of refrigerant and thermal exchange fluid helps maximize heat exchange between the two fluids.

To minimize the force required to insert or remove the Heat Exchange (Hx) Bag or vessel from the Cold Plates, several methods are described below.

The frictional force between the Cold Plates and the Hx Bag may be reduced by adding coating to the surface of the Cold Plates that lowers its coefficient of friction. Possible coatings include Teflon or similar. The surface of the Cold Plates may be polished. A coating may be added to the surface of the Hx Bag that lowers its coefficient of friction, e.g., materials that may be used include silicone, or similar (these can be brushed, sprayed, dipped, etc.)

In some embodiments, a layer (release layer or antifriction layer) of material may be placed over the outside surface of the Hx Bag which lowers its coefficient of friction. Possible materials include paralyene, HDPE (Triton), ePTFE, PTFE, FEP or similar. A low friction sheet made of these materials may be used. In certain embodiments, a fluoropolymer may be placed on the cold plates and use a urethane HX bag with HDPE release layer on the bag. The HX bag may include an HDPE release layer on each side of the bag with each layer and the urethane bag affixed to the cassette frame with pegs or clamps. Alternatively, a single longer piece of HDPE release layer may be folded around the HX bag and then the bag and release layers are affixed to the cassette frame with pegs or clamps

The pulse-damping outflow conduit 30 functions not only as a conduit through which the thermal exchange fluid flows but also a pulse damper for damping pulses in the thermal exchange fluid as it flows through the outflow conduit, to a catheter. Pulses may arise due to the nature of the pump used for the thermal exchange fluid. For example, in the case of a peristaltic pump with two drive rollers, at certain times both drive rollers are in contact with the pump tubing, and at other times only one drive rollers is in contact with the pump tubing, depending on the angular position of the pump rotor within the raceway. The thermal exchange fluid system volume suddenly increases when a roller from the peristaltic pump loses contact with the pump tubing as a normal part of the pump's rotation. This happens because a section of the pump tubing that had been flattened, and had zero cross-sectional area, suddenly becomes round and contains a non-zero cross-sectional area. The increase in system volume is approximately the cross-sectional area of the tubing in its round state multiplied by the length of tubing flattened by the roller. The pulse dampener should have enough flexibility to contract suddenly and decrease its volume by approximately this amount in order to dampen the pulse. For example, the volume gained by the pump tubing when a roller leaves contact with it may be 2 to 3 mL. Therefore it is desirable for a pulse dampener to be able to decrease its volume by this amount with a minimal change in system pressure. The pulse damping conduit may comprise, for example, tubing that has sufficient elastic or flexural properties to dampen, attenuate or reduce the amplitude of pulses in the thermal exchange fluid as it flows therethrough. For example, if the conduit is able to expand by a volume of 20 to 30 mL under 60 psi of pressure, then it will be able to contract by 2 to 3 mL when the pressure drops by approximately 6 psi. The more compliant the conduit is, the smaller the pressure drop that occurs when the tubing contracts, and therefore the better the conduit performs its damping function. While a highly compliant tubing is desirable, at the same time, the conduit should have sufficient mechanical strength to expand and contract by this amount repeatedly without rupture. For example if a peristaltic pump has two driving rollers, turns at 40 RPM, and a procedure lasts for 12 hours, the conduit must withstand 57,600 pulsation cycles. To balance these conflicting requirements, for example, in certain embodiments, the length of the pulse damping conduit may be about 90″ and could range between 20″ and 100″. The conduit may be made of a low durometer polyurethane (Prothane II 65-70A) and have a large ID at 0.25″ and could range between 0.15″ and 0.40″. The wall thickness of the conduit is about 0.094″ and could range between 0.06″ and 0.25″.

As seen in FIGS. 26 and 27 the cassette housing 62 is connected to the frame 69 by a hinged connection 200. As packaged prior to use, the hinged connection 200 is in a closed configuration so that the housing 62 and accompanying pump tubing 65 are folded over the cassette's flexible vessel or bag 63 in the manner seen in FIG. 27. At the time of use, the hinged connection is moved to an open configuration causing the housing 62 and accompanying pump tubing 65 to extend at a substantially right angle relative to the expandable vessel or bag 63, as seen in FIG. 26. The hinged connection 200 locks in such open position so that the cassette 64 cannot be returned to the folded configuration seen in FIG. 27 without removing, disrupting or altering the hinged connection 200. For example, the hinged connection may be unlocked or disengaged by sliding a hinge protrusion forward or backward within a hinge slot, thereby disengaging the lock.

Details of the sensor module 34 are shown in FIG. 29. The sensor module comprises upper and lower housing portions 302 a, 302 b which, in combination, form an enclosed housing. Within the housing there is positioned an electronic storage medium 310 which holds encoded information. Examples of the types of encoded information that may be stored include but are not limited to; unique identifier(s) for the changeable components (e.g., manufacturer identification, part number, lot number, etc.), indications of whether the changeable component(s) have previously been used (e.g., an encoded indication of first use), indications of whether the changeable component(s) is/are expired (e.g., encoded expiration date), operational characteristic(s) of the changeable component(s) (e.g., encoded indications of the size, type, volume, etc. of the changeable component(s). In this non-limiting example, the electronic storage medium comprises electrically erasable programmable read-only memory (EEPROM). One example of how the controller may check to determine whether the components had previously been used is by checking the EEPROM or other data storage medium 310 for a First-Use date. The First-Use date would be “EMPTY” if this is the first time the changeable component (e.g., the cassette assembly) has been connected to a console 14. If the First-Use date is “EMPTY”, the controller will write the current date to the EEPROM's memory location where the First-Use date will then be stored.

Also, within the housing of the sensor module 34, there are provided a first temperature sensor (e.g., a thermistor) for sensing the temperature of thermal exchange fluid flowing to the catheter 12 and a second temperature sensor 300 b (e.g., a second thermistor) for sensing the temperature of thermal exchange fluid returning from the catheter 12. Signals from these first and second temperature sensors 300 a, 300 b, as well as body temperature signals from the connected body temperature sensor TS and encoded data from the electronic storage medium 310, are transmitted through temperature lead TL. A pressure lead PL, which carries signals from a pressure sensor that senses the pressure of thermal exchange fluid within the cassette tubing or console 14, combines with the temperature lead TL, as shown, and the combined leads are connected to the control console 14. In this manner, the controller in the console main housing receives signals indicating a) the encoded data from the electronic storage medium 310, b) subject body temperature, c) thermal exchange fluid temperature flowing to catheter, d) thermal exchange fluid temperature flowing from catheter and e) thermal exchange fluid pressure. The controller may be programmed to use the encoded information and/or sensed temperatures and/or sensed pressure for control of the system 10 and/or for computation/display of data. For example, the controller may be programmed to use the difference between the sensed temperature of thermal exchange fluid flowing to the catheter and the sensed temperature of thermal exchange fluid flowing from the catheter, along with the fluid flow rate or pump speed, to calculate the Power at which the body heat exchanger is operating or the power output of the heat exchanger. Power may be calculated by the following equation: Power(Watts)=(HE Fluid Temp OUT−HE Fluid Temp IN)·Flow Rate·CP

-   -   wherein:     -   HE Fluid Temp IN is the current measured temperature of heat         exchange fluid flowing into the heat exchanger 18;     -   HE Fluid Temp OUT is the current measured temperature of heat         exchange fluid flowing out of the heat exchanger;     -   Flow Rate is the measured or calculated flow rate of heat         exchange fluid through the heat exchanger; and     -   CP is the specific heat capacity of the heat exchange fluid.

Such Power may be displayed on the display or user interface 24. Also, the controller may be programmed to check and accept the encoded information from the electronic storage medium 310 before allowing the system 10 to be used for warming or cooling the body of the subject and/or to adjust operating variable or parameters to suit operative characteristics (e.g., size, operating volume, type) of the catheter 14, cassette 64, temperature probe, tubing or other components. This pre-check of the encoded information may occur in various sequences or processes. One example of a process by which this pre-check may occur is by the following steps:

-   -   1. User connects tubing/cassette/sensor module assembly 60 to         control console 14.     -   2. Console controller detects this connection. Such detection of         the connection may occur by the controller scanning the         temperature sensor channels, which will open channels when no         itubing/cassette/sensor module assembly 60 is connected but will         become non-open when a tubing/cassette/sensor module assembly 60         is connected. Alternatively, this could be done by the         controller polling the polling the pressure sensor in the         cassette 64 or the EEPROM in the sensing module 34 for a         response.     -   3. Controller establishes a secure communication session with         the EEPROM and reads its content. The EEPROM's content may be         encrypted such that it is readable only by a processor having a         secret key. In some embodiments, the EEPROM itself may be         encoded with a secret key such that the controller may establish         a secure session in connection with the sensing module 34.     -   4. In some embodiments, the EEPROM content may comprise the         following information, some or all of which must be checked and         verified/accepted by the controller before priming and operation         of the system 10 may occur:     -   a. Manufacturer ID (factory written)     -   b. Cassette part # (factory written)     -   c. Shelf-life Expiration date (factory written)     -   d. Lot # (factory written)     -   e. Expiration duration since first use (factory written)     -   f. First-Use date (written when the cassette is first plugged         into the console)

FIG. 30 is a schematic diagram of the endovascular heat exchange system 10. This schematic diagram shows major components of the system 10, including the console 14, heat exchange catheter 12, thermal exchange engine 108, console head/user interface 24, thermal exchange plates 80 and cassette 64. Additionally, this schematic diagram includes other components and functional indicators labeled according to the following legend:

FS FLOW, SALINE FW FLOW, WATER LS LEVEL, SALINE LW LEVEL, WATER PSR PRESSURE SWITCH, REFRIGERANT PS PRESSURE, SALINE S SWITCH TACH TECHOMETER TA TEMPERATURE, AIR TR TEMPERATURE, REFRIGERANT TP TEMPERATURE, PLATE TS TEMPERATURE, SALINE TW TEMPERATURE, WATER

To set up the system 10 a new tubing/cassette/sensor module assembly 60 or cassette assembly is obtained and removed from its packaging and the cassette 64 is unfolded to the opened and locked configuration seen in FIG. 26. The access cover 42 of the control console 14 is opened. An “open” button is pressed on the touch screen user interface 24 causing the pump 70 to shift to its loading configuration as seen in FIG. 23. The cassette frame 69 and expandable vessel or bag 63 are inserted downwardly into the cassette receiving space 66 until the housing 62 abuts front plate 172. The pump tubing 165 is inserted within the pump raceway 162. The access cover 42 is then closed and a “close” button is depressed on user interface 24 causing the pump 70 to shift to the operative configuration (FIG. 22). The user then presses a “prime” button on user interface 24 to prime the system with thermal exchange fluid from a bag or other container that has been hung on bracket 48 and connected to the system 10.

After the system has been primed, the catheter 12 is connected and inserted into the subject's body and the system 10 is operated to warm or cool the subject's body as desired.

FIG. 31 is a schematic diagram of an example of a heat exchange system 10 a capable of providing endovascular and/or body surface heat exchange. The system includes all of the elements described in the system 10 of FIG. 30 and, like FIG. 30, includes labeling according to the legend set forth above.

Additionally, this system 10 a includes a body surface heat exchange fluid circuit 400 such that the system can provide body surface heat exchange by circulating warmed or cooled heat exchange fluid through at least one body surface heat exchanger 402 (e.g., a heat exchange pad, blanket, garment, etc.) Such operation of the body surface heat exchange fluid circuit 400 and body surface heat exchanger 402 may be performed in addition to or instead of endovascular heat exchange. The body surface heat exchange fluid circuit includes a fluid reservoir, a pump, a bypass valve, a vent valve, thermal exchange plates and a body surface heat exchange device, e.g., a pad. A fluid, e.g., water, is added to the fluid reservoir. When the bypass valve is closed to the vent valve and open to the bypass line, fluid circulates from the pump, through the body surface fluid chambers in the thermal exchange plates, the reservoir, the bypass valve, and back into the pump. This allows the volume of fluid within the system to come to thermal equilibrium with the thermal exchange plates, which may be useful in preparing the device to deliver temperature management treatment to the patient. In normal operation, the bypass valve is open to the vent valve and the vent valve is closed, and fluid circulates from the pump, through the body surface fluid chambers in the thermal exchange plates, through the reservoir, bypass valve, and vent valve, to the body surface heat exchange device and then back through the pump. To drain the body surface heat exchange device, the vent valve is opened which allows air into the circuit and prevents fluid from flowing from the bypass valve. This forces fluid out of the body surface heat exchange device to the pump. The pump is a positive displacement pump capable of pumping air or liquid through the body surface fluid chambers in the thermal exchange plates, to the reservoir. The reservoir is open to ambient air (to allow excess air to escape the system if introduced by the draining process or normal operation, or to accommodate changes in fluid volume due to thermal expansion) and includes a fill port or drain. The circuit also includes body surface heat exchange fluid temperature sensors to provide feedback to the controller, and fluid temperature sensors and fluid flow sensors for use in power calculations.

In certain embodiments, one or more of the systems described herein may also include one or more physiological alarms and/or technical alarms. The physiological alarms may appear next to the patient's temp on the display screen, and may occur when the patient temperature exceeds the high or low patient temperature alarm value. Technical alarms may appear elsewhere on the display screen and may be triggered by console errors or other events, e.g., probe or catheter disconnection, saline loop overpressure, pump malfunction or open lid, and may be displayed by priority. Any of the alarms may be audible. The system may also transmit data, including patient and/or treatment data wirelessly, e.g., via Wifi, Bluetooth or other wireless connection. Data may also be transmitted via USB, Ethernet or wired connection. The system may be electrically powered or battery powered.

The endovascular temperature management system 10 described in various embodiments herein is a high powered system, capable of rapidly cooling a patient.

In certain embodiments, the cassette/console is designed and configured such that it is capable of delivering ≤4° C. working fluid or saline at a rate of ≥600 mL/min, at steady state, when up to 700 W of heat is added to the working fluid or saline loop (e.g., heat added by the subject's body).

In certain embodiments, the cassette/console is designed and configured such that it is capable of delivering ≤4° C. working fluid or saline at a rate of 220+−20 ml/min, at steady state, when ≤70 W of heat is added to the working fluid or saline loop (e.g., heat added by the subject's body).

In certain embodiments, the cassette/console is designed and configured such that it is capable of delivering ≥42° C. working fluid or saline at a rate of >400 mL/min, at steady state, when up to 200 W of heat is removed from the working fluid or saline loop.

In certain embodiments, the system (cassette, console, and catheter) is designed and configured such that it is capable of delivering greater than 400 Watts, or greater than or equal to 500 Watts, or greater than or equal to 600 Watts of cooling power, e.g., with ≤4° C. working fluid or saline at a catheter pressure of about 60 PSI. In certain embodiments, the system may deliver from 500 to 700 W or 600 to 700 W of cooling power or about 675 W of cooling power or greater than 700 W of cooling power.

In certain embodiments, the system (cassette, console, and catheter) is designed and configured such that it is capable of delivering > or equal to 50 W of warming power e.g., with >37° C. working fluid or saline at a catheter pressure of about 40 PSI.

In certain embodiments, the system performance parameters were verified during a bench test. The bench test included placing a catheter (which is connected to a console/cassette assembly) in a rigid 22 mm ID tube, which simulates the average IVC (inferior vena cava) diameter, through which water at a temperature of 37 degrees C. is flowing at a rate of 2.5 liters per minute (simulating blood flow) over the catheter in a direction from the proximal end of the catheter to the distal end of the catheter.

In certain embodiments, in maintenance and controlled rate warming, the system may control a stable patient's temperature, as measured by console, within about 0.3° C. of target when using a temperature sensor or probe on or in the catheter. During normal use and in the case of a sudden saline loop blockage, the system shall regulate and limit working fluid or saline pressure for catheters as follows: <20 C: 60 psi nominal, 90 psi limit; >=20 C: 40 psi nominal, 70 psi limit; or 40 psi nominal, 70 psi limit. The console working fluid pump and cassette shall be capable of an output up to 600 mL/min at 70 psi. Saline or working fluid pressure at the outlet of the saline pump may be measured, e.g., over a range of 0-100 psi with an accuracy of ±5 psi over the range 10-70 psi. The system may be used concurrently with a defibrillator, electro surgical unit or other device or during an MRI. The console and cassette together may be capable of delivering <8° C. saline, at a rate of ≥600 mL/min, within 5 minutes of turning on the console, when starting with the system equilibrated to ambient temperature. The console and cassette together may be capable of changing the temperature from 4° C. to 40° C. within 10 minutes.

Supplemental Warming by Hot Gas Bypass

With reference to FIG. 34, at least some embodiments of the system 10 may include a hot gas bypass circuit and controller/processor(s) programmed to cause hot refrigerant to circulate from the refrigeration system of the cooling engine 108 through the thermal exchange plates 80 to assist the heaters 82 when conditions are deemed to indicate that such assistance of the heaters 82 is appropriate. When the system 10 requires less cooling than what the cooling engine provides when the compressor is at the minimum speed, the heater(s) 82 are operative to warm the thermal exchange plates 80. An indicator of the warming power output of the heater(s) 82 is monitored. So long as the warming power expended by the heater(s) 82 remains below a predetermined limit, the system 10 will continue to operate with only the heater(s) 82 warming the thermal exchange plates 80. However, if the warming power output of the heater(s) 82 exceeds a predetermined limit, the controller(s) will cause hot refrigerant to circulate from the refrigeration system of the cooling engine 108 through the hot gas bypass circuit and through the thermal exchange plates 80, thereby assisting the heaters 82 in warming the thermal exchange plates 80. The amount of assistance the given to the heaters by the hot gas bypass circuit is determined by the duty cycle of the hot gas bypass being open vs being dosed. When the monitored heater power falls below the predetermined limit, the controller(s) may then incrementally or progressively reduce the hot gas bypass valve duty cycle (BVDC) to facilitate the correct amount of cooling or warming of the subject body temperature to the target temperature without significant overshoot of the target temperature.

To provide incremental or continuous change of the amount of supplemental heating provided by the hot gas bypass, the controller in some embodiments of the system 10 may be programmed to vary duty cycle of the hot gas bypass as the monitored power output of the heater(s) 82 changes. For example, if the maximum heating power output of the heater(s) 82 occurs at a heater duty cycle (HDC) of 30%, the predetermined limit may be set at an HDC of 15% (i.e., one half of the maximum possible heater output). The hot gas bypass circuit may be operative to deliver hot refrigerant to the thermal exchange plates 80 on a hot gas bypass valve duty cycle (BVDC). For example, at a BVDC of 50%, a bypass valve would open for a period of 50 seconds to allow a 50 second flow of hot refrigerant to the thermal exchange plates 80 and would then close for a period of 50 seconds to halt the flow of hot refrigerant to the thermal exchange plates 80 for a subsequent period of 50 seconds, etc. Once the monitored heater power has exceeded the 15% HDC predetermined limit, the controller will trigger the bypass circuit to begin delivering hot refrigerant to the thermal exchange plates 80. Once the flow of hot refrigerant to the thermal exchange plates 80 has commenced, the controller will cause the BVDC to increase as the HDC increases above the 15% HDC predetermined limit and will cause the BVDC to decrease as the HDC decreases below the 15% HDC predetermined limit. There may be a maximum and minimum limit of the BVDC, and the BVDC cannot exceed those limits (e.g., max of 90% and min of 0%).

Combined Variation of Heat Exchange Fluid Flow Rate and Temperature for Precision Maintenance of Target Body Temperature

In some embodiments of the system 10, the controller/processor(s) may be programmed to vary not only the temperature of the heat exchange fluid being circulated through the heat exchange catheter 12, but also the rate and/or frequency of such flow. One non-limiting example of this is shown in the flow diagram of FIG. 35. In this example, after the subject has reached the target temperature and the system 10 is operating to maintain the body temperature at or within a permissible variance range of the target temperature, the system 10 holds the temperature of the heat exchange fluid constant and varies the speed of the pump 70 to adjust the flow rate of heat exchange fluid through the catheter 12 as needed to maintain the body temperature. The controller monitors the pump speed. If the pump speed exceeds a predetermined limit, the controller will then cause warming or cooling of the thermal exchange plates 80 to adjust the temperature of the heat exchange fluid as needed to reduce the pump speed to the predetermined limit. This allows for optimal combination of flow rate and temperature adjustment during the maintenance phase of a treatment session. It is to be understood that this applies only so long as the system is continuing to cool or continuing to warm in order to maintain the body temperature. If it becomes necessary for the system to switch from cooling to warming or from warming to cooling, the controller will adjust the temperature of the heat exchange fluid irrespective of whether the pump speed has exceeded the limit.

For example, after the system 10 has cooled a subject to a target body temperature of 32 degrees C., the subject's body may tend to rewarm. Thus, the system will operate in cooling mode to maintain the target body temperature against the body's inherent tendency to rewarm. In doing so, the system will maintain a constant temperature of heat exchange fluid and will vary the speed of the pump 70 as needed to maintain the target body temperature. However, if it becomes necessary for the pump 70 to run at a speed that exceeds a predetermined limit, the controller will cause the cooling engine 108 to reduce the temperature of the heat exchange fluid by an amount which will allow the pump to slow to a predetermined limit while still maintaining the target body temperature.

Pressure Feedback

As described, the heat exchange catheter system 10 may incorporate pressure sensor(s) for sensing the pressure of the circulating heat exchange fluid. During a given treatment session, over-pressurization events can occur. This is when the saline pressure is above the saline pressure predetermined limit. Such over-pressurization events are typically of a transient nature and result from temporary compression or bending of the catheter 12 or associated tubing, or other causes. During a given treatment session, under-pressurization events can also occur. Such under-pressurization events occur when the Saline Pump Maximum Set Point (SPM_set) is reached, meaning the saline pump is not allowed to move any faster, but the saline pressure is below the saline pressure predetermined limit. When an over-pressurization or under-pressurization event of significant magnitude occurs, it may be desirable to adjust SPM_set. However, it is preferable not to abruptly change or overly reduce/increase the pump speed. Additionally, after a transient over-pressurization or under-pressurization event has past, it is desirable to return the speed of the pump 70 to optimal operating speeds to maintain normal pressurization of the circulating heat exchange fluid.

FIG. 36 is a flow diagram illustrating the SPM_set adjustment protocol that some embodiments of the system 10 may be programmed to perform. The system 10 is equipped to sense the temperature of the heat exchange fluid, and the heat exchange fluid is classified as “cold” or “hot”. In this non-limiting example, the predetermined limit for “cold” heat exchange fluid is set at 60 pounds per square inch (psi) and the predetermined limit for “hot” heat exchange fluid is set at 40 psi. The SPM_set will only be adjust if the saline pressure is above the predetermined limit or the saline pump set point is equal to SPM_set. The controller will cause the SPM_set to decrease if the saline pressure is above the pressure predetermined limit, and will cause the SPM_set to increase as the saline pressure is below the pressure predetermined limit. There may be a maximum and minimum limit of the SPM_set, and the SPM_set cannot exceed those limits (e.g., max of 100% and min of 10%).

Optionally, the controller/processor(s) may also be programmed to store the most recent SPM_set for “cold” and “hot” heat exchange fluids. Thus, when the saline temperature threshold is crossed, the system 10 will switch from “cold” mode to “hot” mode, or vice versa, and upon doing so may recall and apply the recently calculated SPM_set setting for that temperature. In this example, the SPM_set adjustment protocol repeats every three seconds, however other intervals could alternatively be used.

Hypothermic Treatment to Deter Reperfusion Injury

FIG. 26 shows one example of a clinical protocol that may be used to effect rapid hypothermia to deter reperfusion injury in a subject suffering from an ischemic event that may be treated in a manner that causes reperfusion or restoration of blood flow to the ischemic tissue. Non-limiting examples of such reperfursion procedures include angioplasty, stenting, atherectomy, embolectomy, thrombectomy, insertion of a perfusion wire or other conduit to carry blood or oxygenated fluid through or past an obstruction, administration or a thrombolytic agent (e.g., streptokinase or tissue plasminogen activator), some types of surgical revascularization, etc. While reperfusion treatments may restore a flow of blood or other oxygenated fluid to the ischemic tissue, they can also result in significant reperfusion injury which contributes to the amount of tissue that is ultimately infarcted or caused to become necrotic due to the ischemic event. Reperfusion injury is thought to occur in stages. Initially, the ischemia causes increased permeability of capillaries and arterioles. When reperfusion is accomplished, the renewed pressure within those damaged capillaries and arterioles results in diffusion and filtration of fluid into the adjacent tissue. This causes chemical imbalances within the tissue that give rise to an inflammatory response. These events and possibly others result in post-reperfusion damage to the tissue that may be permanent.

As explained herein, the above-described heat exchange catheter system 10 has the unique ability to cool an adult human subject's body to a hypothermic temperature below 34 degrees C., and preferably between 32 degrees C. and 34 degrees C., in approximately 20 minutes. This rapid induction of hypothermia allows caregivers to select an appropriate time to perform the reperfusion procedure after the subjects body temperature has been lowered to the target temperature. Prior studies have indicated that if hypothermia below 35 degrees C. is effected prior to reperfursion, the severity of reperfursion injury, and hence the size or severity of any permanent tissue infarction, is reduced. Applicant has performed a pilot study using the above-described protocol for deterrence of reperfusion injury in human subjects presenting at hospital emergency departments suffering from acute ST elevation myocardial infarction (STEMI). In this pilot study, subjects were randomized into hypothermia and non-hypothermia (control) groups. Subjects in the hypothermia group received standard anti-shivering medication and a heat exchange catheter was placed in the inferior vena cava (IVC). A high power heat exchange catheter system was then used to rapidly cool the body of each subject in the hypothermia group to a temperature below 34 degrees C. within <90 minutes of the subject's arrival in the emergency department. Each subject then underwent percutaneous coronary Intervention (PCI) resulting in reperfusion of the ischemic myocardium. The subjects in the hypothermia group had a body temperatures at the time of reperfusion (i.e., measured at PCI wire crossing) of 33.6+1.0 degrees C.

Following completion of the reperfusion procedure, hypothermia was maintained in each hypothermia group subject for a period of three hours at a target temperature setting of 32 degrees C. Thereafter, the hypothermia group subjects were gradually rewarmed to a body temperature of 36 degrees C.

Four to six days after the event, each subject underwent cardiac magnetic resonance imaging (cMR) and infarct size divided by left ventricular mass (IS/LVM) was determined. On average, subjects in the hypothermia group had a 7.1% absolute change in IS/LVM and approximately a 30% relative reduction compared to the non-hypothermia controls. A 5% absolute change in IS/LVM is generally viewed as a good clinical outcome.

The results of this pilot study, when compared with previously reported data, suggests that 1) cooling of the subject's body temperature at a faster rate (i.e., made possible by using a high cooling power system) results in reduced infarct size measured as IS/LVM, 2) There appears to be a dose-response relationship whereby lower body temperature at the time of reperfusion correlates with greater protection against reperfusion injury and, thus, smaller infarct size.

Accordingly, a method for reducing reperfusion injury in a human or animal subject who undergoes a reperfusion procedure following an ischemic event (e.g., myocardial infarction, acute coronary syndrome, stroke, infarction or ischemia of any metabolic tissue or organ including but not limited to heart, lung, kidney, liver and brain) is provided. In this method, the heat exchange catheter 12 is inserted into the subject's vasculature and the system 10 is used to lower a body temperature of the subject to a temperature below 34 degrees C. and preferably between 32 degrees C. and 34 degrees C. prior to reperfusion. The above described techniques for estimating body temperature at a target location may be utilized in this method and the target location may be in or near the organ or tissue where the ischemia is occurring. For example, in a subject suffering from an evolving myocardial infarction of myocardial ischemia, the system 10 may operate to lower the estimated cardiac temperature (LV Temperature) to the hypothermic temperature. Thereafter, caregivers may perform a reperfusion procedure at a selected time after the body temperature has been cooled to the target hypothermic temperature, thereby deterring reperfusion injury and/or reducing the amount of tissue that ultimately becomes infarcted or necrotic.

Although the invention has been described hereabove with reference to certain examples or embodiments of the invention, various additions, deletions, alterations and modifications may be made to those described examples and embodiments without departing from the intended spirit and scope of the invention. For example, any elements, steps, members, components, compositions, reactants, parts or portions of one embodiment or example may be incorporated into or used with another embodiment or example, unless otherwise specified or unless doing so would render that embodiment or example unsuitable for its intended use. Also, where the steps of a method or process have been described or listed in a particular order, the order of such steps may be changed unless otherwise specified or unless doing so would render the method or process unsuitable for its intended purpose. Additionally, the elements, steps, members, components, compositions, reactants, parts or portions of any invention or example described herein may optionally exist or be utilized in the absence or substantial absence of any other element, step, member, component, composition, reactant, part or portion unless otherwise noted. All reasonable additions, deletions, modifications and alterations are to be considered equivalents of the described examples and embodiments and are to be included within the scope of the following claims. 

What is claimed is:
 1. A system comprising: an endovascular heat exchange catheter which comprises (i) a catheter body having a distal end, (ii) an elongated member attached to the catheter body and extending beyond the distal end of the catheter body, and (iii) at least one helically coiled tube disposed on the elongated member and connected to delivery and return lumens in the catheter body; and a fluid cooling apparatus comprising a refrigeration apparatus, heat exchange plates, and a cassette connected to the delivery and return lumens of the catheter body and operative to cause circulation of a cooled thermal exchange fluid through the cassette, into the catheter body, through said at least one helically coiled tube, out of the catheter body and back into the cassette, wherein the heat exchange plates each comprise a refrigerant flow channel that is serpentine or convoluted and configured to be secured in a vertical orientation with respect to gravity during operation, the refrigerant flow channel configured to cause refrigerant to evaporate while flowing through the refrigerant flow channel to generate at least about 600 watts of cooling power; wherein the endovascular heat exchange catheter, fluid cooling apparatus and said at least one helically coiled tube are sized, configured and constructed to render the system capable of delivering the at least about 600 watts of cooling power when i) the endovascular heat exchange catheter is inserted in a vasculature of a human patient such that blood flows through the vasculature and past said at least one helically coiled tube and ii) the fluid cooling apparatus is being operated to cause said circulation, thereby resulting in exchange of heat between the cooled thermal exchange fluid circulating through said at least one helically coiled tube and blood flowing through the vasculature and past said at least one helically coiled tube.
 2. A system according to claim 1 wherein the fluid cooling apparatus is configured to deliver, to the endovascular heat exchange catheter, a flow of thermal exchange fluid that is cooled to a temperature at or below 4° C. at a rate of at least 600 mL/min at steady state, when up to 700 W of heat is being added to the flow of thermal exchange fluid as a result of heat exchange through a heat exchanger of the endovascular heat exchange catheter.
 3. A system according to claim 1 wherein the fluid cooling apparatus are configured to deliver to the endovascular heat exchange catheter a flow of thermal exchange fluid that is cooled to a temperature at or below 4° C. at a rate of from 200 mL/min to 240 mL/min at steady state, when up to 70 W of heat is being added to the flow of thermal exchange fluid as a result of heat exchange through a heat exchanger of the endovascular heat exchange catheter.
 4. system according to claim 1 further comprising a heating apparatus useable for warming rather than cooling the thermal exchange fluid.
 5. A system according to claim 1 wherein the system is configured to deliver greater than or equal to 600 W of cooling power by circulating thermal exchange fluid that is cooled to a temperature at or below 4° C. through the endovascular heat exchange catheter at a catheter pressure of about 60 PSI.
 6. A system according to claim 4 wherein the fluid cooling apparatus and the heating apparatus are configured to deliver to the endovascular heat exchange catheter a flow of thermal heat exchange fluid that is warmed to a temperature at or above 42° C. at a rate of at least 400 mL/min at steady state, when up to 200 W of heat is being removed from the flow of thermal exchange fluid as a result of heat exchange through a heat exchanger of the endovascular heat exchange catheter.
 7. system according to claim 4 configured to deliver greater than or equal to 50 W of warming power by circulating thermal exchange fluid that is warmed to a temperature above 37° C. through the endovascular heat exchange catheter at a catheter pressure of about 40 PSI.
 8. A system according to claim 1 wherein the cooling apparatus includes a pump for circulating the thermal exchange fluid through the cassette, into the catheter body, through said at least one helically coiled tube, out of the catheter body and back into the cassette.
 9. A system according to claim 8 further comprising a controller which is programmed to selectively vary both a temperature and flow rate of the thermal exchange fluid to maintain a body temperature of the human patient at or within a permissible range of a target body temperature.
 10. A system according to claim 9 wherein the controller is programmed such that, after a body temperature of the human patient has reached a target temperature, the controller will cause the system to maintain said body temperature at or within a permissible variance range of a target temperature by performing steps which comprise: holding constant the temperature of the thermal exchange fluid and varying operation of the pump to adjust a flow rate of the thermal exchange fluid as needed to maintain said body temperature at or within a permissible variance range of the target temperature so long as a pump speed of the pump does not exceed a maximum pump speed; and if the pump exceeds the maximum pump speed, adjusting the temperature of the thermal exchange fluid such that said body temperature is maintained at, or within a permissible variance range of, the target temperature without exceeding the maximum pump speed.
 11. A system according to claim 9 further comprising heating apparatus useable for warming rather than cooling the thermal exchange fluid such that the system may alternately operate in a cooling mode or a warming mode, and wherein, to switch between the cooling mode and the warming mode in order to maintain said body temperature at, or within a permissible variance range of, the target body temperature, the controller is configured to adjust the temperature of the thermal exchange fluid irrespective of whether the maximum pump speed is exceeded.
 12. A system comprising: an endovascular heat exchange catheter which comprises (i) a catheter body having a distal end, (ii) a elongate member attached to the catheter body and extending beyond the distal end of the catheter body, and (iii) at least one helically coiled tube disposed on the elongate member and connected to delivery and return lumen in the catheter body; a fluid cooling apparatus which comprises: a refrigeration apparatus, cooling members having channels through which refrigerant circulates so as to cool the cooling members, wherein the cooling members each comprise a refrigerant flow channel that is serpentine or convoluted and configured to be secured in a vertical orientation with respect to gravity during operation, the refrigerant flow channel configured to cause refrigerant to evaporate while flowing through the refrigerant flow channel to generate at least about 600 watts of cooling power; a cassette having a thermal exchange fluid circulation flow path formed therein, said cassette being connected or connectable to the delivery and return lumens of the catheter body and positionable in proximity to the cooling members; and a pump operative to cause circulation of thermal exchange fluid through the cassette where the thermal exchange fluid becomes cooled by the cooling members, into the catheter body, through the at least one helically coiled tube, out of the catheter body, and back through the cassette where the thermal exchange fluid becomes cooled by the cooling members; wherein the endovascular heat exchange catheter, refrigeration apparatus, cooling members, cassette and pump are configured to render the system capable of delivering the at least about 600 watts of cooling power when i) the endovascular heat exchange catheter is inserted in vasculature of a human patient such that blood flows through the vasculature and past said at least one helically coiled tube and ii) the fluid cooling apparatus is being operated to cause said circulation, thereby resulting in exchange of heat between the thermal exchange fluid that is cooled and circulating through the at least one helically coiled tube and blood flowing through the vasculature and past said at least one helically coiled tube.
 13. A system according to claim 12 wherein the cooling members comprise cooling plates.
 14. A system according to claim 12 wherein the refrigeration apparatus, cooling members, cassette and pump are configured to deliver to the endovascular heat exchange catheter a flow of heat exchange fluid that is cooled to a temperature at or below 4° C. at a rate of at least 600 mL/min at steady state, when up to 700 W of heat is being added to the flowing thermal exchange fluid as a result of heat exchange through a heat exchanger of the endovascular heat exchange catheter.
 15. A system according to claim 12 wherein the refrigeration apparatus, cooling members, cassette and pump are configured to deliver to the endovascular heat exchange catheter a flow of thermal exchange fluid that is cooled to a temperature at or below 4° C. at a rate of from 200 mL/min to 240 mL/min at steady state, when up to 70 W of heat is being added to the flowing thermal exchange fluid as a result of heat exchange through a heat exchanger of the endovascular heat exchange catheter.
 16. A system according to claim 12 wherein the refrigeration apparatus, thermal exchange members, cassette and pump are configured to deliver greater than or equal to 600 W of cooling power by circulating thermal exchange fluid that is cooled to a temperature at or below 4° C. through the endovascular heat exchange catheter at a catheter pressure of about 60 PSI.
 17. A system according to claim 12 further comprising heating apparatus useable for warming rather than cooling the thermal exchange fluid.
 18. A system according to claim 17 wherein the heating apparatus, cassette and pump are configured to deliver to the endovascular heat exchange catheter a flow of thermal exchange fluid that is warmed to a temperature at or above 42° C. at a rate of at least 400 mL/min at steady state, when up to 200 W of heat is being removed from the flowing thermal exchange fluid as a result of heat exchange through a heat exchanger of the endovascular heat exchange catheter.
 19. A system according to claim 18 configured to deliver greater than or equal to 50 W of warming power by circulating thermal exchange fluid that is warmed to a temperature above 37° C. through the endovascular heat exchange catheter at a catheter pressure of about 40 PSI.
 20. A system according to claim 12 further comprising a controller which is programmed to selectively vary both the temperature and flow rate of the thermal exchange fluid to maintain a body temperature of the human patient at, or within a permissible range of, a target body temperature. 